CN207317579U - Heat exchange pipe mechanism in blast furnace gas heat exchange device - Google Patents

Heat exchange pipe mechanism in blast furnace gas heat exchange device Download PDF

Info

Publication number
CN207317579U
CN207317579U CN201721280258.7U CN201721280258U CN207317579U CN 207317579 U CN207317579 U CN 207317579U CN 201721280258 U CN201721280258 U CN 201721280258U CN 207317579 U CN207317579 U CN 207317579U
Authority
CN
China
Prior art keywords
heat
gas
blast furnace
heat exchange
tube bundle
Prior art date
Legal status (The legal status is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the status listed.)
Active
Application number
CN201721280258.7U
Other languages
Chinese (zh)
Inventor
孙健
崔磊
胡法议
Current Assignee (The listed assignees may be inaccurate. Google has not performed a legal analysis and makes no representation or warranty as to the accuracy of the list.)
Suzhou Hailu Heavy Industry Co Ltd
Original Assignee
Suzhou Hailu Heavy Industry Co Ltd
Priority date (The priority date is an assumption and is not a legal conclusion. Google has not performed a legal analysis and makes no representation as to the accuracy of the date listed.)
Filing date
Publication date
Application filed by Suzhou Hailu Heavy Industry Co Ltd filed Critical Suzhou Hailu Heavy Industry Co Ltd
Priority to CN201721280258.7U priority Critical patent/CN207317579U/en
Application granted granted Critical
Publication of CN207317579U publication Critical patent/CN207317579U/en
Active legal-status Critical Current
Anticipated expiration legal-status Critical

Links

Landscapes

  • Heat-Exchange Devices With Radiators And Conduit Assemblies (AREA)

Abstract

The utility model discloses the heat exchange pipe mechanism in a kind of blast furnace gas heat exchange device, including:First group of heat-exchanging tube bundle and second group of heat-exchanging tube bundle, first group of heat-exchanging tube bundle and second group of U-shaped arrangement of heat-exchanging tube bundle, the both ends of first group of heat-exchanging tube bundle are the first gas inlet end and the first gas exit end respectively, the both ends of second group of heat-exchanging tube bundle are the second gas inlet end and the second gas exit end respectively, first gas exit end is connected by turning flue with the second gas inlet end, blast furnace gas enters first group of heat-exchanging tube bundle by the first gas inlet end, then entered to from the first gas exit end in turning flue, blast furnace gas in turning flue is entered in second group of heat-exchanging tube bundle from the second gas inlet end, discharged again from the second gas exit end afterwards.The utility model increases the heated length of blast furnace gas significantly so that the heating effect of blast furnace gas greatly improves, so as to carry out abundant guarantee for the power generation by waste combustion in later stage.

Description

Heat exchange pipe mechanism in blast furnace gas heat exchange device
Technical field
It the utility model is related to blast furnace gas heat exchange device technical field.
Background technology
Steel mill has some processes flow to produce the byproducts such as blast furnace gas, and the exhaust gas volumn of blast furnace gas is big, and calorific value is low, needs It is re-fed into after certain temperature is heated in blast furnace gas heat exchange device to gas furnace power generation by waste combustion.Current blast furnace gas heat exchange There are following defect for device:First, heat exchanger tube length is limited, so as to cause blast furnace gas heating effect poor.2nd, the flue gas of blast furnace gas Amount is big, and carries dust particles, and not only input end is produced and is washed away, but also very easily disorderly in the input end generation of heat exchanger tube Stream, so as to increase resistance of the coal gas in heat exchanger tube.
Utility model content
The utility model technical issues that need to address are:A kind of heating effect that can effectively improve blast furnace gas is provided, And heat exchanger tube of the blast furnace gas in heat exchanger tube in the blast furnace gas heat exchange device of resistance can be effectively reduced.
To solve the above problems, the technical solution adopted in the utility model is:Heat exchanger tube machine in blast furnace gas heat exchange device Structure, including:Heat-exchanging tube bundle, the heat-exchanging tube bundle include arranged in parallel two groups --- first group of heat-exchanging tube bundle and second Group heat-exchanging tube bundle, first group of heat-exchanging tube bundle and second group of U-shaped arrangement of heat-exchanging tube bundle, the both ends difference of first group of heat-exchanging tube bundle It is the first gas inlet end and the first gas exit end, the both ends of second group of heat-exchanging tube bundle are the second gas inlet end and respectively Two gas exit ends, the first gas exit end are connected by turning flue with the second gas inlet end, and blast furnace gas is by first Gas inlet end enters first group of heat-exchanging tube bundle, is then entered to from the first gas exit end in turning flue, in turning flue Blast furnace gas entered to from the second gas inlet end in second group of heat-exchanging tube bundle, afterwards again from the second gas exit end discharge.
Further, the heat exchange pipe mechanism in foregoing blast furnace gas heat exchange device, wherein, the first gas inlet end and Be mounted on introducing pipe on the mouth of pipe of the every heat exchanger tube at two gas inlet ends, it is each introduce pipe by it is outer and in port be respectively Outer intake and interior intake, each internal diameter for introducing pipe are directed inwardly into mouth by outer intake and are gradually reduced until and heat exchange tube Mouthful outside diameter it is consistent, tube wall between outer intake and interior intake is in projecting inward so as to guiding from outside to inside to pipe is introduced Cambered surface.
Further, the heat exchange pipe mechanism in foregoing blast furnace gas heat exchange device, wherein, the first gas exit end and It is mounted on the fairlead of cone cylinder shape shape on the mouth of pipe of the every heat exchanger tube at two gas exit ends, each fairlead is by inner and outer Port is respectively that interior outlet and outer outlet, the internal diameter of each fairlead gradually increase by the outside outlet of interior outlet, The interior outlet of fairlead is identical with the outside diameter of the heat exchanger tube mouth of pipe.
Further, the heat exchange pipe mechanism in foregoing blast furnace gas heat exchange device, wherein, each outer introducing for introducing pipe The bore of mouth is 1.5~2 times of interior intake bore.
Further, the heat exchange pipe mechanism in foregoing blast furnace gas heat exchange device, wherein, the outer extraction of each fairlead The bore of mouth is 1.5~2 times of interior outlet bore.
Further, the heat exchange pipe mechanism in foregoing blast furnace gas heat exchange device, wherein, every of every group of heat-exchanging tube bundle The mouth of pipe at heat exchanger tube both ends welds after stretching out the outer 10~12mm of tube sheet with fairlead or introducing pipe.
The utility model has the advantages that:First, the U-shaped arrangement of heat-exchanging tube bundle, this is compact-sized, and required space is small, and The heated length of blast furnace gas is increased significantly, and the heating effect of blast furnace gas greatly improves, so that the power generation by waste combustion for the later stage Carry out abundant guarantee.2nd, the mouth of pipe of the heat exchanger tube at the first gas inlet end and the second gas inlet end is respectively mounted introducing pipe, its Good guiding function can be played to blast furnace gas, blast furnace gas is greatly reduced into the resistance in heat exchanger tube, so as to effective Reduce generation turbulent in heat exchanger tube;Meanwhile it is each introduce pipe can also highly desirable avoid the weld bonds of exchanger tubes and tubesheets by To washing away for the blast furnace gas with dust particles, so as to substantially increase the security of blast furnace gas heat exchange device operation.3rd, The mouth of pipe of the every heat exchanger tube at one gas exit end and the second gas exit end is respectively provided with fairlead, and which greatly enhances blast furnace Smooth degree when coal gas is discharged from heat exchanger tube, so as to effectively avoid turbulent generation, greatly reduces blast furnace gas in heat exchanger tube The resistance of operation.
Brief description of the drawings
Fig. 1 is the structure diagram of the heat exchange pipe mechanism in the blast furnace gas heat exchange device.
Fig. 2 is attachment structure schematic diagram of the heat exchanger tube with introducing pipe.
Fig. 3 is the attachment structure schematic diagram of heat exchanger tube and fairlead.
Embodiment
The utility model is described in further detail with preferred embodiment below in conjunction with the accompanying drawings.
As shown in Figure 1, the heat exchange pipe mechanism in blast furnace gas heat exchange device, including:Heat-exchanging tube bundle, the heat-exchanging tube bundle bag Include arranged in parallel two groups --- first group of heat-exchanging tube bundle 1 and second group of heat-exchanging tube bundle 2, first group of heat-exchanging tube bundle and second The group U-shaped arrangement of heat-exchanging tube bundle.The both ends of first group of heat-exchanging tube bundle 1 are that the first gas inlet end 11 and the first coal gas go out respectively Mouthful end 12, the both ends of second group of heat-exchanging tube bundle 2 are the second gas inlet end 21 and the second gas exit end 22 respectively, the first coal gas The port of export 12 is connected by turning flue 3 with the second gas inlet end 21.Blast furnace gas running orbit is U-shaped, specifically It is as follows:Blast furnace gas is entered in first group of heat-exchanging tube bundle 1 by the first gas inlet end 11, then from the first gas exit end 12 into Enter into turning flue 3, the blast furnace gas in turning flue 3 enters to second group of heat-exchanging tube bundle 2 from the second gas inlet end 21 In, discharged again from the second gas exit end 21 afterwards.The U-shaped arrangement of heat-exchanging tube bundle, this is compact-sized, and required space is small, And the heated length of blast furnace gas is increased significantly, blast furnace gas is sufficiently heated to required temperature in U-shaped operational process Degree, heating effect greatly improves, so as to carry out abundant guarantee for the power generation by waste combustion in later stage.
In the present embodiment, on the mouth of pipe of the every heat exchanger tube 4 at the first gas inlet end 11 and the second gas inlet end 21 It is mounted on introducing pipe 5.The mouth of pipe at every 4 both ends of heat exchanger tube welds after stretching out the outer 10~12mm of tube sheet 7 with introducing pipe 5.Often It is a introduce pipe 5 by it is outer and in port be respectively outer intake 51 and interior intake 52, the internal diameter of introducing pipe 5 is by outer intake 51 Mouth 52 is directed inwardly into be gradually reduced up to consistent with the outside diameter of 4 mouth of pipe of heat exchanger tube, between outer intake 51 and interior intake 52 Tube wall be in introduce the projecting inward cambered surface 53 so as to guide from outside to inside of pipe 5.The mouth of each outer intake 51 for introducing pipe 5 Footpath is 1.5~2 times of interior 52 bore of intake.First gas inlet end 11 and the heat exchanger tube 4 at the second gas inlet end 21 The mouth of pipe be respectively mounted introduce pipe 5, it can play blast furnace gas good guiding function, greatly reduce blast furnace gas enter heat exchange Resistance in pipe 4, so as to effectively reduce generation turbulent in heat exchanger tube 4.In addition, it is worth noting that each introduce pipe 5 also The weld bond of heat exchanger tube 4 and tube sheet 7 can be highly desirable avoided to be subject to washing away for the blast furnace gas with dust particles, so that significantly Improve the security of blast furnace gas heat exchange device operation.
In the present embodiment, on the mouth of pipe of the every heat exchanger tube 4 at the first gas exit end 12 and the second gas exit end 22 Be mounted on the fairlead 6 of cone cylinder shape shape, the mouth of pipe at every 4 both ends of heat exchanger tube stretch out after the outer 10~12mm of tube sheet 7 with extraction Pipe 6 connects.Fairlead 6 is respectively that interior outlet 61 and outer outlet 62, the internal diameter of fairlead 6 are drawn by interior by inner and outer port Export 61 outside outlets 62 gradually to increase, the interior outlet 61 of fairlead 6 is identical with the outside diameter of 4 mouth of pipe of heat exchanger tube.Each draw The bore of the outer outlet 62 of outlet pipe 6 is 1.5~2 times of interior 61 bore of outlet.First gas exit end 12 and second The mouth of pipe of the every heat exchanger tube 4 at gas exit end 22 is respectively provided with fairlead 6, which greatly enhances blast furnace gas from heat exchanger tube 4 Smooth degree during discharge, so as to effectively avoid turbulent generation, greatly reduces the resistance that blast furnace gas is run in heat exchanger tube 4.Often 4 both ends of root heat exchanger tube are mounted with introducing pipe 5 and fairlead 6 respectively, this is with regard to that can greatly reduce fortune of the blast furnace gas in heat exchanger tube 4 Row resistance, effectively avoids turbulent generation.

Claims (6)

1. the heat exchange pipe mechanism in blast furnace gas heat exchange device, including:Heat-exchanging tube bundle, it is characterised in that:The heat-exchanging tube bundle bag Include arranged in parallel two groups --- first group of heat-exchanging tube bundle and second group of heat-exchanging tube bundle, first group of heat-exchanging tube bundle and second group The U-shaped arrangement of heat-exchanging tube bundle, the both ends of first group of heat-exchanging tube bundle are the first gas inlet end and the first gas exit end respectively, The both ends of second group of heat-exchanging tube bundle are the second gas inlet end and the second gas exit end respectively, and the first gas exit end is by turning Curved flue is connected with the second gas inlet end, and blast furnace gas enters first group of heat-exchanging tube bundle by the first gas inlet end, then Entered to from the first gas exit end in turning flue, the blast furnace gas in turning flue enters to from the second gas inlet end In two groups of heat-exchanging tube bundles, discharged again from the second gas exit end afterwards.
2. the heat exchange pipe mechanism in blast furnace gas heat exchange device according to claim 1, it is characterised in that:First gas inlet Be mounted on introducing pipe on the mouth of pipe of the every heat exchanger tube at end and the second gas inlet end, it is each introduce pipe by it is outer and in end Mouthful be respectively outer intake and interior intake, each internal diameter for introducing pipe by outer intake be directed inwardly into mouth be gradually reduced up to The outside diameter of the heat exchanger tube mouth of pipe is consistent, and the tube wall between outer intake and interior intake is in projecting inward so as to by outer to pipe is introduced The cambered surface guided inwards.
3. the heat exchange pipe mechanism in blast furnace gas heat exchange device according to claim 1 or 2, it is characterised in that:First coal gas The fairlead of cone cylinder shape shape is mounted on the mouth of pipe of the port of export and the every heat exchanger tube at the second gas exit end, it is each to draw Guan Youli and outer port are respectively that interior outlet and outer outlet, the internal diameter of each fairlead are outwards drawn by interior outlet Gradually increase, the interior outlet of fairlead are identical with the outside diameter of the heat exchanger tube mouth of pipe for mouth.
4. the heat exchange pipe mechanism in blast furnace gas heat exchange device according to claim 2, it is characterised in that:Each introducing pipe The bore of outer intake is 1.5~2 times of interior intake bore.
5. the heat exchange pipe mechanism in blast furnace gas heat exchange device according to claim 3, it is characterised in that:Each fairlead The bore of outer outlet is 1.5~2 times of interior outlet bore.
6. the heat exchange pipe mechanism in blast furnace gas heat exchange device according to claim 2, it is characterised in that:Every group of heat-exchanging tube bundle The mouth of pipe at every heat exchanger tube both ends stretch out after the outer 10~12mm of tube sheet with fairlead or introducing pipe welding.
CN201721280258.7U 2017-09-30 2017-09-30 Heat exchange pipe mechanism in blast furnace gas heat exchange device Active CN207317579U (en)

Priority Applications (1)

Application Number Priority Date Filing Date Title
CN201721280258.7U CN207317579U (en) 2017-09-30 2017-09-30 Heat exchange pipe mechanism in blast furnace gas heat exchange device

Applications Claiming Priority (1)

Application Number Priority Date Filing Date Title
CN201721280258.7U CN207317579U (en) 2017-09-30 2017-09-30 Heat exchange pipe mechanism in blast furnace gas heat exchange device

Publications (1)

Publication Number Publication Date
CN207317579U true CN207317579U (en) 2018-05-04

Family

ID=62428517

Family Applications (1)

Application Number Title Priority Date Filing Date
CN201721280258.7U Active CN207317579U (en) 2017-09-30 2017-09-30 Heat exchange pipe mechanism in blast furnace gas heat exchange device

Country Status (1)

Country Link
CN (1) CN207317579U (en)

Cited By (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107643007A (en) * 2017-09-30 2018-01-30 苏州海陆重工股份有限公司 Heat exchange pipe mechanism in blast furnace gas heat exchange device

Cited By (2)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
CN107643007A (en) * 2017-09-30 2018-01-30 苏州海陆重工股份有限公司 Heat exchange pipe mechanism in blast furnace gas heat exchange device
CN107643007B (en) * 2017-09-30 2024-02-23 苏州海陆重工股份有限公司 Heat exchange tube mechanism in blast furnace gas heat exchanger

Similar Documents

Publication Publication Date Title
CN202141195U (en) Vacuum hot water boiler with waste heat recycling device
CN102620578B (en) Flue gas waste heat recycling device
CN104930531A (en) Exhaust heat recovery and dust removal integrated type biomass boiler
CN105570956B (en) A kind of residual heat from boiler fume circulating heat supply system
CN207317579U (en) Heat exchange pipe mechanism in blast furnace gas heat exchange device
CN202691998U (en) Automatic dust removal type waste heat boiler
CN207175469U (en) A kind of Flue Gas of Nonferrous Smelting relieving haperacidity high-temperature residual heat utilization device
CN107643007A (en) Heat exchange pipe mechanism in blast furnace gas heat exchange device
CN203848696U (en) Heat accumulating type settling chamber waste heat storage device
CN206753667U (en) A kind of gas turbine exhaust gas water conservancy diversion, fairing
CN202432887U (en) Novel flue gas waste heat recovery device
CN207674977U (en) A kind of glass furnace waste-heat recovery device
CN206695625U (en) A kind of built-in sintering machine large flue waste heat boiler device
CN206410564U (en) High-temperature flue gas heat recoverer
CN206724723U (en) Casting furnace waste-heat recovery device
CN206037008U (en) Gas boiler
CN206919710U (en) Energy-saving heat exchanger
CN205425774U (en) Device is recycled to dry bed steam
CN218210896U (en) Waste gas and waste heat recycling device of setting machine
CN213902019U (en) Energy-saving device for recycling heat energy in production process of dimethyl succinylsuccinate
CN209197528U (en) Gas waste-heat recover
CN220907528U (en) Environment-friendly smoke exhaust device for hot blast stove
CN209101852U (en) A kind of coal gasification heat-exchanger rig
CN206018696U (en) Expansion type tube case of air preheater
CN102759092A (en) Device for recycling waste heat generated in procedure of acid making and conversion of sulphide ore

Legal Events

Date Code Title Description
GR01 Patent grant
GR01 Patent grant